JPH08127814A - Heat treatment for steel - Google Patents

Heat treatment for steel

Info

Publication number
JPH08127814A
JPH08127814A JP26853194A JP26853194A JPH08127814A JP H08127814 A JPH08127814 A JP H08127814A JP 26853194 A JP26853194 A JP 26853194A JP 26853194 A JP26853194 A JP 26853194A JP H08127814 A JPH08127814 A JP H08127814A
Authority
JP
Japan
Prior art keywords
heat treatment
gas
furnace
nitrogen gas
treatment furnace
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP26853194A
Other languages
Japanese (ja)
Other versions
JP2929068B2 (en
Inventor
Masaaki Hashimoto
正明 橋本
Terukazu Kanda
輝一 神田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Iwatani International Corp
Kanto Yakin Kogyo Co Ltd
Original Assignee
Iwatani International Corp
Kanto Yakin Kogyo Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Iwatani International Corp, Kanto Yakin Kogyo Co Ltd filed Critical Iwatani International Corp
Priority to JP26853194A priority Critical patent/JP2929068B2/en
Publication of JPH08127814A publication Critical patent/JPH08127814A/en
Application granted granted Critical
Publication of JP2929068B2 publication Critical patent/JP2929068B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE: To perform heat treatment of steel without decarburizing and carburizing by controlling the addition amount of hydrocarbon gas based on the concentration of methane in the exhaust gas exhausted from a heat treatment furnace. CONSTITUTION: A work W of low carbon steel, etc., is held in a heat treatment furnace 1 and nonoxidizing gas is introduced, and heating treatment is done in this atmosphere. At this time, nitrogen gas is supplied via a nitrogen gas supply route 7 while raising the temp. in the heat treatment furnace 1, and the atmosphere in the furnace chamber is replaced with the nitrogen gas. When the temp. in the furnace 1 reaches the prescribed temp., the flow rate of the nitrogen gas to be supplied into the heat treatment furnace 1 is reduced, and hydrocarbon gas, e.g. propylene gas, having 2-4 carbon atoms and double bond is added to the nitrogen gas via a gas supply route 8 and supplied into the heat treatment furnace 1. The additive quantity of this hydrocarbon gas is controlled based on the methane concentration in the exhaust gas exhausted from the heat treatment furnace 1. By this method, the necessity of a gas generator can be obviated, and cost reduction can be attained.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、炭素鋼や炭素合金鋼等
の鉄鋼を熱処理方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat treatment method for steel such as carbon steel and carbon alloy steel.

【0002】[0002]

【従来技術】従来、鋼の熱処理は、ワークを収容した熱
処理炉を窒素ガスでパージしながら昇温し、熱処理炉内
の温度が所定温度に達すると、パージ用窒素ガスの供給
を止めるとともに、変成炉ガスを熱処理炉内に供給して
熱処理炉内を変成炉ガス雰囲気に維持し、この変成炉ガ
ス雰囲気中でワークを所定温度に加熱し、ワークを所定
温度で一定時間保持し、所定の冷却速度で熱処理をして
いた。
2. Description of the Related Art Conventionally, in heat treatment of steel, the temperature of a heat treatment furnace containing a work is increased while purging with nitrogen gas, and when the temperature in the heat treatment furnace reaches a predetermined temperature, supply of nitrogen gas for purging is stopped and The metamorphic furnace gas is supplied into the heat treatment furnace to maintain the metamorphic furnace gas atmosphere in the heat treatment furnace, the work is heated to a predetermined temperature in the metamorphic furnace gas atmosphere, and the work is held at the predetermined temperature for a predetermined time, The heat treatment was performed at the cooling rate.

【0003】[0003]

【発明が解決しようとする課題】ところが、従来の熱処
理方式では、熱処理炉内に充満させるガスを変成炉発生
ガスで形成していたことから、変成炉の維持管理が面倒
である。また、球状化焼鈍のようなA1変態点域では処
理中に熱処理炉に撹拌モータ軸部分及びシール部分など
から外気が侵入すると、爆発する危険性があり、熱処理
炉などの気密性の確保が面倒であるとともに、エンリッ
チ方式で酸素計、二酸化炭素計によるカーボンコントロ
ール制御が困難であった。本発明はこのような点に着目
して窒素ガスベースで熱処理する方法を提供するもので
ある。
However, in the conventional heat treatment method, the gas for filling the heat treatment furnace is formed by the gas generated by the shift converter furnace, so that the maintenance of the shift converter furnace is troublesome. Also, in the A1 transformation point region such as spheroidizing annealing, there is a risk of explosion if outside air enters the heat treatment furnace from the agitating motor shaft portion and seal portion during processing, and it is troublesome to secure airtightness in the heat treatment furnace. In addition, it was difficult to control the carbon by the oxygen meter and the carbon dioxide meter by the enrichment method. The present invention provides a method for heat treatment based on nitrogen gas, paying attention to such a point.

【0004】[0004]

【課題を解決するための手段】上述の目的を達成するた
めに本発明は、熱処理炉内を窒素ガスでパージしながら
昇温し、炉内温度が所定温度に達すると、熱処理炉内に
供給する窒素ガスの流量を減少させるとともに、炭素数
2〜4で二重結合を有する炭化水素系ガスを窒素ガスに
添加して熱処理炉内に供給し、この炭化水素ガスの添加
量を熱処理炉から排出される排ガス中のメタン濃度に基
づき炉内雰囲気を制御するように構成したことを特徴と
している。
Means for Solving the Problems In order to achieve the above-mentioned object, the present invention increases the temperature in a heat treatment furnace while purging with nitrogen gas, and when the temperature in the heat treatment furnace reaches a predetermined temperature, it is supplied into the heat treatment furnace. The flow rate of the nitrogen gas to be reduced is reduced, and a hydrocarbon-based gas having 2 to 4 carbon atoms and having a double bond is added to the nitrogen gas and supplied into the heat treatment furnace, and the addition amount of this hydrocarbon gas is changed from the heat treatment furnace. It is characterized in that the atmosphere in the furnace is controlled based on the methane concentration in the exhaust gas discharged.

【0005】[0005]

【作用】本発明では、熱処理炉内を窒素ガスでパージし
ながら昇温し、炉内温度が所定温度に達すると、熱処理
炉内に供給する窒素ガスの流量を減少させるとともに、
炭素数2〜4で二重結合を有する炭化水素系ガスを窒素
ガスに添加して熱処理炉内に供給し、この炭化水素系ガ
スの添加量を熱処理炉から排出される排ガス中のメタン
濃度に基づき炉内雰囲気を制御するように構成している
ので、ワーク中の炭素量のコントロールは低温度で分解
する炭素数2〜4で二重結合を有する炭化水素系ガスを
用い、外乱として炉壁や炉壁の間隙から侵入した酸素や
水分と炭化水素系ガスとを反応させて一酸化炭素を生成
することにより行う。
In the present invention, the temperature inside the heat treatment furnace is increased while purging with nitrogen gas, and when the temperature inside the furnace reaches a predetermined temperature, the flow rate of nitrogen gas supplied into the heat treatment furnace is reduced and
A hydrocarbon-based gas having 2 to 4 carbon atoms and having a double bond is added to nitrogen gas and supplied into the heat treatment furnace, and the addition amount of this hydrocarbon-based gas is adjusted to the methane concentration in the exhaust gas discharged from the heat treatment furnace. Since it is configured to control the atmosphere in the furnace based on this, the control of the carbon content in the work uses a hydrocarbon-based gas having a double bond with a carbon number of 2 to 4 that decomposes at a low temperature, and the furnace wall The reaction is performed by reacting oxygen or water that has entered through the gap between the furnace wall and the furnace gas with the hydrocarbon gas to generate carbon monoxide.

【0006】[0006]

【実施例】図1はベル型炉を使用して焼鈍する装置の概
略図であり、符号(1)はベル型炉で形成した熱処理炉で
あり、この熱処理炉(1)の底部に撹拌ファン(2)が配置
してあり、この撹拌ファン(2)のファン軸(3)は熱処理
炉(1)の底壁(4)を貫通して炉外に突出している。
EXAMPLE FIG. 1 is a schematic view of an apparatus for annealing using a bell-type furnace. Reference numeral (1) is a heat treatment furnace formed in the bell-type furnace, and a stirring fan is provided at the bottom of the heat treatment furnace (1). (2) is arranged, and the fan shaft (3) of the stirring fan (2) penetrates the bottom wall (4) of the heat treatment furnace (1) and projects outside the furnace.

【0007】また、熱処理炉(1)の底壁(4)には、雰囲
気ガス導入口(5)と雰囲気ガス導出口(6)とが形成して
あり、雰囲気ガス導入口(5)には窒素ガス供給路(7)と
添加用炭化水素ガス供給路(8)を合流させて接続させて
ある。窒素ガス供給路(7)は流量調節可能な開閉弁(9)
と流量計(10)を介して窒素ガスボンベ等の窒素ガス源(1
1)に接続してあり、添加用炭化水素系ガス供給路(8)は
流量調節弁(12)と流量計(13)を介して添加用炭化水素系
ガス容器(14)に接続してある。なお、添加用炭素水素系
ガスとしては、プロピレンが使用されている。
At the bottom wall (4) of the heat treatment furnace (1), an atmosphere gas inlet (5) and an atmosphere gas outlet (6) are formed, and the atmosphere gas inlet (5) is The nitrogen gas supply passage (7) and the addition hydrocarbon gas supply passage (8) are joined together and connected. The nitrogen gas supply channel (7) has an on-off valve (9) with adjustable flow rate.
And a nitrogen gas source (1
1), and the addition hydrocarbon-based gas supply passage (8) is connected to the addition hydrocarbon-based gas container (14) via the flow rate control valve (12) and the flow meter (13). . In addition, propylene is used as the carbon-hydrogen-based gas for addition.

【0008】一方、雰囲気ガス導出口(6)からの排気ガ
ス路(15)には、オリフィス(16)が配置してあり、このオ
リフィス(16)よりも上流側部分から分岐導出させた分析
用ガス導出管(17)が分析計(18)に接続している。そし
て、この分析計(18)で分析検出したメタンガス濃度に基
づき、添加用炭化水素系ガス供給路(8)に配置した流量
調節弁(12)の開閉度を調節するようにしてある。
On the other hand, an orifice (16) is arranged in the exhaust gas passage (15) from the atmosphere gas outlet (6), and the orifice is branched from the upstream side of the orifice (16) for analysis. A gas outlet pipe (17) is connected to the analyzer (18). Then, based on the methane gas concentration analyzed and detected by the analyzer (18), the opening / closing degree of the flow rate control valve (12) arranged in the addition hydrocarbon-based gas supply passage (8) is adjusted.

【0009】このような構成による熱処理炉での焼鈍操
作の手順を以下に説明する。処理するワーク(W)を熱処
理炉(1)内にセットする。このワークのセット時に炉室
内は大気雰囲気になり、また炉壁内には大気や水蒸気が
侵入している。そしてこのまま昇温すると、この大気中
の酸素の影響でワーク表面が酸化することになるから、
熱処理炉(1)内を昇温しながら、窒素ガス供給路(7)か
ら窒素ガスを供給して、炉室内の大気を窒素ガスで置換
する。
The procedure of the annealing operation in the heat treatment furnace having such a structure will be described below. The work (W) to be treated is set in the heat treatment furnace (1). At the time of setting this work, the inside of the furnace is in an atmospheric atmosphere, and the atmosphere and water vapor have entered the inside of the furnace wall. And if the temperature is raised as it is, the surface of the work will be oxidized by the influence of oxygen in the atmosphere,
While heating the inside of the heat treatment furnace (1), nitrogen gas is supplied from the nitrogen gas supply passage (7) to replace the atmosphere in the furnace chamber with nitrogen gas.

【0010】炉室内が残留酸素濃度100ppm 程度の窒
素雰囲気となり、炉室内の温度がプロピレンの分解温度
である550℃程度になると、窒素ガス供給路(7)の開
閉弁(9)を絞ってその流量を半減させるとともに、添加
用炭化水素系ガス供給路(8)の流量調整弁(12)を調節開
弁して、プロピレンガスを窒素ガスに1%程度添加した
状態で熱処理炉(1)内に供給する。
When the inside of the furnace becomes a nitrogen atmosphere having a residual oxygen concentration of about 100 ppm and the temperature inside the furnace reaches about 550 ° C., which is the decomposition temperature of propylene, the on-off valve (9) of the nitrogen gas supply passage (7) is throttled. In the heat treatment furnace (1), reduce the flow rate by half and open the flow rate control valve (12) of the hydrocarbon gas supply passage (8) for addition to adjust the propylene gas to 1% nitrogen gas. Supply to.

【0011】図2に示す熱処理パターンに基づき、この
プロピレンガスを1%添加した窒素ガスの供給を継続し
た状態でワークをA1変態温度よりも20℃程度高い温
度に10時間程度維持し、その後ゆっくりと冷却して、
ワークを焼鈍する。
Based on the heat treatment pattern shown in FIG. 2, the work was kept at a temperature about 20 ° C. higher than the A1 transformation temperature for about 10 hours while continuously supplying the nitrogen gas added with 1% of propylene gas, and then slowly. And cool
Anneal the work.

【0012】この高温維持期間に、撹拌ファン軸(3)の
挿通部分等からわずかに外気が侵入するが、このとき、
酸素や水分等の酸化性ガスが炉内に存在すると、プロピ
レンは次のように反応して一酸化炭素ガスと水素ガスを
生成し、ワークの脱炭を防止する。
[0012] During this high temperature maintaining period, a small amount of outside air enters from the portion where the stirring fan shaft (3) is inserted, but at this time,
When an oxidizing gas such as oxygen or water exists in the furnace, propylene reacts as follows to generate carbon monoxide gas and hydrogen gas, and prevents decarburization of the work.

【化1】 Embedded image

【0013】一方、高温維持期間中に、炉内の酸化性ガ
ス量がなくなると、プロピレンは次のように分解してメ
タンガスを生成する。
On the other hand, when the amount of oxidizing gas in the furnace is exhausted during the high temperature maintaining period, propylene decomposes as follows to produce methane gas.

【化2】 そしてこのカーボン量が多くなると、ワーク表面から浸
炭することになる。
Embedded image When the amount of carbon increases, the work surface is carburized.

【0014】このため、排気ガス中のメタンガス量を分
析検出し、そのメタンガス量に基づき、添加用炭化水素
ガス供給路(8)での流量調整弁(12)の開弁量調節して、
窒素ガスへのプロピレンガス添加量を調整する。そし
て、炉の気密度にもよるが、プロピレンガスの添加量が
2%をこえると、上記式の分解がおこり、ワークの表
面に浸炭が見られ、炉壁にも遊離炭素の付着が見られ
た。また、プロピレンの添加量が1%を切ると、ワーク
の表面に脱炭が見られた。この結果、焼鈍作業でプロピ
レンの添加量を1〜2%に制御することが望ましい。な
お、プロピレンの添加量を調整することにより、浸炭処
理や脱炭処理を行うこともできる。
Therefore, the amount of methane gas in the exhaust gas is analyzed and detected, and the opening amount of the flow rate adjusting valve (12) in the addition hydrocarbon gas supply passage (8) is adjusted based on the amount of methane gas,
Adjust the amount of propylene gas added to nitrogen gas. And, depending on the airtightness of the furnace, when the amount of propylene gas added exceeds 2%, the above formula is decomposed, carburization is observed on the surface of the work, and free carbon is observed to adhere to the furnace wall. It was Further, when the amount of propylene added fell below 1%, decarburization was observed on the surface of the work. As a result, it is desirable to control the addition amount of propylene to 1 to 2% in the annealing work. In addition, carburizing treatment or decarburizing treatment can be performed by adjusting the addition amount of propylene.

【0015】上記実施例では、添加する炭化水素をプロ
ピレンガスとしたが、エチレンガスを使用するようにし
てもよい。この場合、ワークの加熱温度よりも低温で分
解する炭化水素が必要となるから、炭素数2から炭素数
4で分解しやすい二重結合を有する炭化水素が最適であ
るが、プロパンやエタン等の二重結合を有しない炭化水
素であってもよい。
Although propylene gas is used as the hydrocarbon to be added in the above embodiment, ethylene gas may be used. In this case, a hydrocarbon that decomposes at a temperature lower than the heating temperature of the work is required. Therefore, a hydrocarbon having a double bond that easily decomposes with 2 to 4 carbon atoms is optimal, but propane, ethane, or the like. It may be a hydrocarbon having no double bond.

【0016】[0016]

【発明の効果】本発明では、熱処理炉内を窒素ガスでパ
ージしながら昇温し、炉内温度が所定温度に達すると、
熱処理炉内に供給する窒素ガスの流量を減少させるとと
もに、炭素数2〜4で二重結合を有する炭化水素系ガス
を窒素ガスに添加して熱処理炉内に供給し、この炭化水
素系ガスの添加量を熱処理炉から排出される排ガス中の
メタン濃度に基づき制御するように構成しているので、
炉内に残存している酸素や水分と炭化水素系ガスとを反
応させて一酸化炭素を生成してワーク中の炭素量のコン
トロールすることができ、炭化水素ガスの添加量により
脱炭処理や浸炭処理、あるいは脱炭又は浸炭することな
しに熱処理できる。しかも、その場合、窒素ガスに炭化
水素系ガスを微量添加するだけであることから、従来の
変成炉ガスを使用するものに比べて安全面で優れている
うえ、変成炉を必要としない分だけ構造が簡素化され、
変成炉の維持管理も必要ないので、ランニングコストも
低下させることかできる。
According to the present invention, the temperature in the heat treatment furnace is raised while purging with nitrogen gas, and when the temperature in the furnace reaches a predetermined temperature,
While reducing the flow rate of nitrogen gas supplied into the heat treatment furnace, a hydrocarbon-based gas having a carbon number of 2 to 4 and having a double bond is added to the nitrogen gas and supplied into the heat treatment furnace. Since the addition amount is controlled based on the methane concentration in the exhaust gas discharged from the heat treatment furnace,
The amount of carbon in the work can be controlled by reacting oxygen and moisture remaining in the furnace with hydrocarbon-based gas to control the amount of carbon in the work. It can be heat treated without carburizing or decarburizing or carburizing. Moreover, in that case, since only a small amount of hydrocarbon gas is added to nitrogen gas, it is superior in safety compared to the one using conventional metamorphic furnace gas, and only the part that does not require a metamorphic furnace is used. The structure is simplified,
The maintenance cost of the converter is not required, so the running cost can be reduced.

【図面の簡単な説明】[Brief description of drawings]

【図1】焼鈍装置の一例を示す概略図である。FIG. 1 is a schematic view showing an example of an annealing device.

【図2】熱処理パターンを示す時間−温度関係グラフで
ある。
FIG. 2 is a time-temperature relationship graph showing a heat treatment pattern.

【符号の説明】[Explanation of symbols]

W…ワーク、1…熱処理炉。 W ... Work, 1 ... Heat treatment furnace.

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 低炭素鋼や低炭素合金鋼からなるワーク
(W)を収容した熱処理炉(1)の内部に非酸化性ガスを注
入し、非酸化性ガス雰囲気中で加熱処理する鋼の熱処理
方法において、熱処理炉(1)を窒素ガスでパージしなが
ら昇温し、炉内温度が所定温度に達すると、熱処理炉
(1)に供給する窒素ガスの流量を減少させるとともに、
炭素数2〜4で二重結合を有する炭化水素系ガスを窒素
ガスに添加して熱処理炉(1)内に供給し、この炭化水素
ガスの添加量を熱処理炉(1)から排出される排ガス中の
メタン濃度に基づき制御するように構成した鋼の熱処理
方法。
1. A work made of low carbon steel or low carbon alloy steel.
In a heat treatment method for steel in which a non-oxidizing gas is injected into the heat treating furnace (1) containing (W) and heat treatment is performed in a non-oxidizing gas atmosphere, the heat treating furnace (1) is purged with nitrogen gas. When the temperature rises and the temperature inside the furnace reaches the specified temperature, the heat treatment furnace
While reducing the flow rate of nitrogen gas supplied to (1),
Exhaust gas discharged from the heat treatment furnace (1) by adding a hydrocarbon gas having 2 to 4 carbon atoms and having a double bond to nitrogen gas and supplying the gas into the heat treatment furnace (1) A method for heat treatment of steel configured to be controlled based on the concentration of methane in the steel.
【請求項2】 窒素ガスへの炭化水素系ガスの添加量を
1〜2%に制御することにより、ワーク(W)を脱炭も浸
炭も起こすことなく熱処理する請求項1に記載の鋼の熱
処理方法。
2. The steel according to claim 1, wherein the work (W) is heat-treated without decarburization or carburization by controlling the addition amount of the hydrocarbon gas to the nitrogen gas to be 1 to 2%. Heat treatment method.
【請求項3】 窒素ガスへの炭化水素系ガスの添加量を
1%未満に制御することにより、ワーク(W)の表面を脱
炭する請求項1に記載の鋼の熱処理方法。
3. The heat treatment method for steel according to claim 1, wherein the surface of the work (W) is decarburized by controlling the amount of the hydrocarbon gas added to the nitrogen gas to be less than 1%.
【請求項4】 窒素ガスへの炭化水素ガス系の添加量を
2%以上に制御することにより、ワーク(W)の表面を浸
炭する請求項1に記載の鋼の熱処理方法。
4. The heat treatment method for steel according to claim 1, wherein the surface of the work (W) is carburized by controlling the amount of the hydrocarbon gas system added to the nitrogen gas to 2% or more.
JP26853194A 1994-11-01 1994-11-01 Heat treatment method for steel Expired - Fee Related JP2929068B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26853194A JP2929068B2 (en) 1994-11-01 1994-11-01 Heat treatment method for steel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26853194A JP2929068B2 (en) 1994-11-01 1994-11-01 Heat treatment method for steel

Publications (2)

Publication Number Publication Date
JPH08127814A true JPH08127814A (en) 1996-05-21
JP2929068B2 JP2929068B2 (en) 1999-08-03

Family

ID=17459815

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2016121962A (en) * 2014-12-25 2016-07-07 オリエンタルエンヂニアリング株式会社 Oxygen sensor calibration system and oxygen sensor calibration method
TWI580792B (en) * 2016-05-09 2017-05-01 中國鋼鐵股份有限公司 Method of reducing decarbonization of surface of carbon-containing steel slab at high temperature

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2016121962A (en) * 2014-12-25 2016-07-07 オリエンタルエンヂニアリング株式会社 Oxygen sensor calibration system and oxygen sensor calibration method
TWI580792B (en) * 2016-05-09 2017-05-01 中國鋼鐵股份有限公司 Method of reducing decarbonization of surface of carbon-containing steel slab at high temperature

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